JP3038338B2 - Vertical firing furnace - Google Patents
Vertical firing furnaceInfo
- Publication number
- JP3038338B2 JP3038338B2 JP4313900A JP31390092A JP3038338B2 JP 3038338 B2 JP3038338 B2 JP 3038338B2 JP 4313900 A JP4313900 A JP 4313900A JP 31390092 A JP31390092 A JP 31390092A JP 3038338 B2 JP3038338 B2 JP 3038338B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- bridge
- hot gas
- space
- furnace
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は石灰石やドロマイトなど
の塊状原料を焼成するための竪型焼成炉に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vertical firing furnace for firing massive raw materials such as limestone and dolomite.
【0002】[0002]
【従来の技術】従来のこの種の竪型焼成炉においては、
例えば外筒と内筒の間に形成された断面円環状の原料通
路に、焼成に供せられる石灰石等の原料を充填させて原
料充填層を形成させ、原料充填層を下降させつつ原料通
路に下方から上方に向けて熱ガスを流して、熱ガスによ
り石灰石等の原料焼成させると共に、熱ガスの一部を原
料充填層から原料通路に面する内筒の壁面に設けた熱ガ
ス流出口を通して該原料充填層外である内筒の内部に取
り出して排熱回収を行わせ、焼成炉としての熱効率を向
上させることが行われている。2. Description of the Related Art In a conventional vertical firing furnace of this kind,
For example, a raw material passage having an annular cross section formed between the outer cylinder and the inner cylinder is filled with a raw material such as limestone to be subjected to firing to form a raw material packed layer, and the raw material passage is formed while lowering the raw material packed layer. A hot gas is caused to flow upward from below, and the raw material such as limestone is fired by the hot gas, and a part of the hot gas is passed through a hot gas outlet provided on the wall surface of the inner cylinder facing the raw material passage from the raw material packed bed. It has been practiced to take out the heat inside the inner cylinder outside of the raw material packed bed and to recover the exhaust heat, thereby improving the thermal efficiency as a firing furnace.
【0003】図4は上記のような従来構造の竪型焼成炉
の熱ガス取出部の要部の構成を説明するものである。図
4において、1は内筒、2は原料通路、3は内筒1の壁
面に形成された熱ガス流出口、4は原料通路2内に充填
された石灰石等の原料、Aは原料通路2内に形成された
原料充填層、Bは原料充填層外を示し内筒1の内部、G
は原料充填層A内を上昇して熱ガス流出口3から流出さ
れる熱ガスを示す。FIG. 4 illustrates the structure of a main part of a hot gas extracting section of a vertical firing furnace having a conventional structure as described above. In FIG. 4, 1 is an inner cylinder, 2 is a raw material passage, 3 is a hot gas outlet formed on the wall surface of the inner cylinder 1, 4 is a raw material such as limestone filled in the raw material passage 2, A is a raw material passage 2 B indicates the outside of the raw material packed layer, and B indicates the outside of the raw material packed layer.
Denotes a hot gas rising in the raw material packed layer A and flowing out from the hot gas outlet 3.
【0004】このような熱ガス流出口3の部分の構成に
おいて、熱ガスGは炉内の原料通路2内の原料4の充填
された原料充填層Aを上昇して来て熱ガス流出口3を通
り、原料充填層A外である内筒1の内部に図示の矢印の
ごとく流れる。このとき熱ガスはその流れに原料中のダ
ストを同伴して熱ガス流出口3を通り内筒1内に流入す
る。内筒1内に流入した熱ガスは炉の外部に取り出され
て燃焼空気の予熱用等に使用される。In such a configuration of the hot gas outlet 3, the hot gas G rises in the raw material packed bed A filled with the raw material 4 in the raw material passage 2 in the furnace, and the hot gas G And flows inside the inner cylinder 1 outside the raw material packed layer A as shown by the arrow in the figure. At this time, the hot gas flows into the inner cylinder 1 through the hot gas outlet 3 with the dust in the raw material accompanying the flow. The hot gas flowing into the inner cylinder 1 is taken out of the furnace and used for preheating combustion air.
【0005】[0005]
【発明が解決しようとする課題】この熱ガス流出口3の
部分においては、原料はその安息角RAにより図示した
ように熱ガス流出口3の下面3a側に張り出して安息角
面3bを形成する。従って、熱ガスはこの安息角面3b
を通って内筒1の内部に流出する。前記の熱ガスに同伴
されるダストの量はガスの流速に比例するが、ガス流速
の最大部分は前記原料安息角面3bの部分となり、原料
充填層A外の内筒1内のBが流速の最低部分となる。こ
のため、原料安息角面3bを通過した部分で熱ガスに同
伴されるダスト量は飽和以上に達し、ダストはガス流中
に浮遊および沈降を起こし、図中にDで示すように堆積
ダストとなって正常なガスの流れを阻害する。At the hot gas outlet 3, the material protrudes toward the lower surface 3a side of the hot gas outlet 3 as shown in the drawing by its repose angle RA to form a repose angle surface 3b. . Therefore, the hot gas is supplied to the repose angle surface 3b.
Through the inner cylinder 1. The amount of dust entrained in the hot gas is proportional to the flow velocity of the gas, but the maximum part of the gas flow velocity is the part of the raw material repose angle surface 3b, and B in the inner cylinder 1 outside the raw material packed bed A is flow velocity. Is the lowest part of For this reason, the amount of dust entrained by the hot gas in the portion that has passed through the material repose angle surface 3b has reached saturation or more, and the dust floats and settles in the gas flow, and as shown by D in the drawing, the dust And interfere with normal gas flow.
【0006】このような現象は普通に焼成を行っている
原料の場合にも問題となるが、特に粉化率の高い結晶組
成をもつ原料を焼成する場合には著しく発生し、ガス流
れの阻害はもとより焼成炉の操業が不可能になり操業を
中断し、堆積したダストの除去作業を余儀なくされてい
る。[0006] Such a phenomenon is also a problem in the case of a raw material which is normally fired, but it occurs remarkably when a raw material having a crystal composition with a high powdering rate is fired, and the gas flow is hindered. In addition, the operation of the kiln has become impossible, and the operation has been interrupted, forcing the removal of accumulated dust.
【0007】本発明は以上のような従来の欠点を除去す
るためになされたものであり、熱ガス流出口の部分に堆
積するダストを円滑に排出させて熱ガス流出口から熱ガ
スが円滑に流出しうるようにした竪型焼成炉を提供する
ことを目的としている。SUMMARY OF THE INVENTION The present invention has been made to eliminate the above-mentioned drawbacks of the prior art, and smoothly discharges dust accumulated at a hot gas outlet so that hot gas flows smoothly from the hot gas outlet. It is an object of the present invention to provide a vertical firing furnace capable of flowing out.
【0008】[0008]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明は、外筒と、炉の上部から下部にかけて該
外筒の中央部に懸垂されて設けられた内筒とにより二重
円筒構造にされ、該外筒と内筒との間が焼成空間として
の円環状断面の原料通路とされてなり、該原料通路内で
原料充填層を下降させつつ下方からバーナで発生される
熱ガスを上昇させ向流接触させて原料の焼成を行うと共
に、熱ガスを該原料通路に面して該内筒の壁面に形成さ
れ該熱ガス発生バーナよりも所定距離上方に位置した熱
ガス流出口を通して原料充填層から内筒の内部である原
料充填層外へ取り出すようにした竪型焼成炉において、
該熱ガス流出口の上部分の原料通路にブリッジを設け、
該ブリッジ自体にはその下部分にブリッジ内部空間を形
成し、該ブリッジによって該ブリッジの下方には該ブリ
ッジ内部空間の下方に引き続いて原料空間部を形成さ
せ、該ブリッジ内部空間と該原料空間部の両空間部が該
熱ガス流出口と連通される状態に構成し、該バーナで発
生された熱ガスは、原料通路の原料充填層を下方から上
方へ向けて流されて該ブリッジの下方の原料空間部にダ
ストを伴って排出され、その後、該ブリッジ内部空間の
天井面に衝突して該熱ガス流出口へ流れうる構成にし
た。SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides an outer cylinder and an upper and lower parts of the furnace.
Double with the inner cylinder suspended from the center of the outer cylinder
It has a cylindrical structure, and the space between the outer cylinder and the inner cylinder is a firing space.
Which will be a raw material passage annular cross-section of, while lowering the material packed layer increases the <br/> heat gas generated by the burner from below by countercurrent contact and fired raw material in the raw material passage with the hot gas to the surface in the material passage is formed on the wall surface of the inner cylinder
In a vertical firing furnace which is to be taken out of the raw material packed bed which is inside the inner cylinder from the raw material packed bed through a hot gas outlet located a predetermined distance above the hot gas generating burner ,
A bridge is provided in a raw material passage at an upper portion of the hot gas outlet,
The bridge itself has an internal space in the lower part of the bridge.
Form, the yellowtail below the bridge by the bridge
Following below the Tsu di inner space to form a source space portion constitutes a state in which two spaces of the bridge interior space and raw material space portion communicates with the heat gas outlet, originating in the burner
The generated hot gas passes through the raw material packed bed in the raw material passage from below.
To the raw material space below the bridge.
Discharge with the strike, and then
The structure was such that it could collide with the ceiling surface and flow to the hot gas outlet .
【0009】[0009]
【作用】炉の上方から下方にかけて形成された外筒と内
筒の間の円環状断面の焼成空間としての原料通路におい
て、それ自体の下部分に内部空間を形成されたブリッジ
が取付けられる。そして、該原料通路において、該ブリ
ッジ内部空間に引き続いてブリッジ下部にはブリッジの
作用によって原料安息角面が形成されることにより原料
空間部が形成される。内筒壁面に形成され熱ガス発生バ
ーナよりも所定距離上方に位置した熱ガス流出口は該ブ
リッジ内部空間と該原料空間部の両空間部に連通され
る。該バーナで発生された熱ガスは、該原料通路の原料
充填層を下方から上方へ向けて流され、ブリッジ下部に
形成される該原料空間部に該原料安息角面を通過して排
出されることになるため、該熱ガスに同伴されて浮遊す
るダストは該原料安息角面を通過してその上面に沈降し
て堆積することになる。また、該熱ガスは該原料空間部
に排出された後、該ブリッジの内部空間に入り、その天
井面に衝突して該熱ガス流出口へと流される。このた
め、該熱ガスに同伴されるダストの一部は該天井面への
衝突により失速し該原料安息角面に沈降、堆積すること
により、熱ガス流出口側へ流れるダスト量が効果的に減
少される。 そして、ブリッジ内部空間はブリッジ自体に
形成されてそれ自体熱ガス流出口へ連通されるため、原
料充填層から熱ガス流出口へと流れる熱ガスの流通(排
出)通路が、ブリッジ自体によってブリッジ下方に形成
される原料安息角面でなる原料空間部と相俟って、確実
に、かつ、広い容積でもって確保され、熱ガスは確実に
熱ガス流出口へ排出される。該原料安息角面に堆積した
ダストは原料の下降と共に炉の底部へ下降して炉外へ排
出される。以上のことにより、熱ガスは熱ガス流出口か
ら内筒内の原料充填層外へ円滑に流出され、焼成炉は連
続して操業される。[Function] An outer tube and an inner tube formed from the upper part to the lower part of the furnace.
Raw material passage as firing space of annular cross section between cylinders
Bridge with an internal space formed in the lower part of itself
Is attached. And, in the material passage,
Subsequent to the inner space of the bridge, a raw material repose angle portion is formed at the lower portion of the bridge by the action of the bridge to form a raw material space portion. A hot gas generation chamber formed on the inner cylinder wall
Hot gas outlet located at a predetermined distance above the over Nah 該Bu
It communicates with both spaces of the ridge inner space and the material space. The hot gas generated by the burner feeds the raw material in the raw material passage.
The packed bed is flowed upward from the bottom, and under the bridge
Since the raw material space is formed and discharged through the material repose angle surface, the dust floating along with the hot gas passes through the material repose angle surface and settles on the upper surface thereof. Deposits. The hot gas is supplied to the raw material space.
After being discharged into the bridge, it enters the interior space of the bridge and
The gas collides with the well surface and flows to the hot gas outlet. others
Therefore, part of the dust entrained by the hot gas
Stall due to collision and settle and accumulate on the material repose angle
Effectively reduces the amount of dust flowing to the hot gas outlet side
Will be reduced. And the bridge internal space is in the bridge itself
Because it is formed and communicates with the hot gas outlet itself,
Of hot gas flowing from the bed to the hot gas outlet (discharge)
Out) A passage is formed below the bridge by the bridge itself
In combination with the raw material space that
And a large volume to ensure that the hot gas
It is discharged to the hot gas outlet. The dust deposited on the repose angle of the raw material descends to the bottom of the furnace with the lowering of the raw material and is discharged out of the furnace. By the above, the hot gas is smoothly flow to the raw material packed layer outside the inner cylinder from the opening out hot gas stream, burning furnace is operated continuously.
【0010】[0010]
【実施例】次に、図面に示した実施例により本発明を詳
細に説明する。図1は本発明の竪型焼成炉の全体構造を
示す縦断面図、図2は図1の熱ガス流出口部の要部拡大
縦断面図であり図3のII〜II線矢視断面図、図3は
図2のIII〜III線矢視断面図である。なお、これ
ら図において、図4と同一部分には同一符号を用いる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail with reference to the embodiments shown in the drawings. FIG. 1 is a longitudinal sectional view showing the entire structure of the vertical firing furnace of the present invention, and FIG. 2 is an enlarged longitudinal sectional view of a main part of a hot gas outlet of FIG. 1 and a sectional view taken along the line II-II in FIG. 3 is a sectional view taken along the line III-III in FIG. In these figures, the same parts as those in FIG.
【0011】図1において、竪型焼成炉の本体は外筒6
の中央部に炉の頂部に支持されて内筒1が懸垂されて設
けられて二重円筒構造とされており、外筒6と内筒1と
の間には焼成空間としての円環状断面の原料通路2が形
成されている。外筒6には前記原料通路2に開口された
熱ガス排出口を有した上段バーナ8と下段バーナ9がそ
れぞれ円周方向に等間隔で複数個ずつ(本実施例では5
箇所ずつ)設けられている。焼成を被る石灰石等の原料
は炉の頂部の矢印10で示す位置から原料通路2に投入
され、この原料通路2内では上から下にかけて原料充填
層Aが形成され、原料は前記上段バーナ8と下段バーナ
9で発生されて上昇する熱ガスと向流接触されて焼成さ
れる。In FIG. 1, the main body of the vertical firing furnace is an outer cylinder 6.
The inner cylinder 1 is suspended from the center of the furnace and supported by the top of the furnace to form a double cylindrical structure. The outer cylinder 6 and the inner cylinder 1 have an annular cross-section as a firing space. A raw material passage 2 is formed. The outer cylinder 6 is provided with a plurality of upper burners 8 and lower burners 9 each having a hot gas discharge port opened in the raw material passage 2 at equal intervals in the circumferential direction (in this embodiment, 5 burners).
Locations). A raw material such as limestone to be fired is introduced into the raw material passage 2 from a position indicated by an arrow 10 at the top of the furnace, and a raw material packed layer A is formed in the raw material passage 2 from top to bottom. The hot gas generated by the lower burner 9 is brought into countercurrent contact with the rising hot gas and fired.
【0012】炉の底部には製品取出口11が設けられて
おり、焼成された製品としての生石灰が取り出される。
12、13はそれぞれ上段バーナ8、下段バーナ9の上
部の原料通路2内で該バーナ12、13と同数設けられ
内筒1と外筒6を連結する連結部材である。A product outlet 11 is provided at the bottom of the furnace to take out quicklime as a fired product.
Reference numerals 12 and 13 denote connecting members which are provided in the same number as the burners 12 and 13 in the raw material passage 2 above the upper burner 8 and the lower burner 9, respectively, and connect the inner cylinder 1 and the outer cylinder 6.
【0013】しかして、上段バーナ8の上部の連結部材
12の上部の原料通路2に面する内筒1の壁面には熱ガ
ス流出口7が開口されて設けられている。この熱ガス流
出口7は円周方向に等角度間隔で複数箇所(図示では1
箇所だが、本実施例では5箇所)形成されており、前記
上段バーナ8と数を同数にして平面視で隣合う上段バー
ナ8と上段バーナ8の中間に位置されるようにして設け
られている。そして、このそれぞれの熱ガス流出口7の
上部分の原料通路2にこは原料通路2を横断して通路2
の全幅にわたってブリッジ5が取付けられている。A hot gas outlet 7 is provided on the wall surface of the inner cylinder 1 facing the raw material passage 2 above the connecting member 12 above the upper burner 8. The hot gas outlets 7 are provided at a plurality of locations (1 in the figure) at equal angular intervals in the circumferential direction.
However, the number of the upper burners 8 is the same as that of the upper burners 8, and the upper burners 8 are provided in the middle of the upper burners 8 adjacent to each other in plan view. . The raw material passage 2 at the upper portion of each of the hot gas outlets 7 is traversed across the raw material passage 2 and
Are mounted over the entire width of the bridge.
【0014】熱ガス流出口7から内筒1の内部に流入し
た熱ガスはその上部から炉外へ排出されてレキュペレー
タ14に導入され、ここでブロワ15により供給される
空気と熱交換される。加熱された空気は前記上段バーナ
8、下段バーナ9に供給される。また、レキュペレータ
14で熱交換に供された熱ガスは排気ファン17によっ
てサイクロン等の脱塵装置16へ導かれてここでダスト
を捕集され大気中へ排出される。The hot gas flowing into the inner cylinder 1 from the hot gas outlet 7 is discharged out of the furnace from the upper portion thereof and introduced into the recuperator 14 where it is exchanged with the air supplied by the blower 15. The heated air is supplied to the upper burner 8 and the lower burner 9. Further, the hot gas provided for heat exchange in the recuperator 14 is guided by an exhaust fan 17 to a dust removing device 16 such as a cyclone, where the dust is collected and discharged to the atmosphere.
【0015】熱ガス流出口7の部分についてさらに詳し
く説明する。上記熱ガス流出口7部において取付けられ
たブリッジ5は、詳細を図2、図3に示すように形成さ
れている。即ち、ブリッジ5は耐火煉瓦で構築され、図
3に示すように円周方向に所定の幅を有し、その断面形
状は頂部が尖って上部に二等辺三角形の斜辺に相当する
急斜面5aが形成され急斜面5aに連ならせて垂直部5
bが形成されている。ブリッジ5自体の下部分は図3に
示すように抉られて両側に袖5c、5cが形成され、そ
の内部には空間Sbが形成されている。そして、図2に
示すように袖5cの下端縁は円弧状に形成され、耐火煉
瓦で形成されるブリッジ5の内筒1と外筒6の間におけ
る保持強度を向上させている。The hot gas outlet 7 will be described in more detail. The bridge 5 attached at the hot gas outlet 7 is formed as shown in detail in FIGS. That is, the bridge 5 is constructed of refractory bricks, has a predetermined width in the circumferential direction as shown in FIG. 3, and has a steep slope 5a corresponding to the hypotenuse of an isosceles triangle at the top with a sharp top. The vertical part 5 is connected to the steep slope 5a.
b is formed. As shown in FIG. 3, the lower part of the bridge 5 itself is hollowed to form sleeves 5c and 5c on both sides, and a space Sb is formed inside. As shown in FIG. 2, the lower end edge of the sleeve 5c is formed in an arc shape to improve the holding strength between the inner cylinder 1 and the outer cylinder 6 of the bridge 5 formed of refractory brick.
【0016】図3において、原料4はブリッジ5の上部
から急斜面5aに沿って流下し滞留を防止される。そし
て、原料はさらに垂直面5bに沿って流下し、垂直面5
bの下端に至るとそこを起点として安息角面3bを形成
して下降する。従って、ブリッジ5自体の下方には両側
の安息角面3b、3bによって原料空間Smが形成され
る。従って、原料空間Sは、この空間Smと前記ブリッ
ジ5の内部の空間Sbとで形成される。In FIG. 3, the raw material 4 flows down from the upper part of the bridge 5 along the steep slope 5a to prevent stagnation. Then, the raw material further flows down along the vertical surface 5b,
When it reaches the lower end of b, it forms the angle of repose 3b starting from there and descends. Therefore, a raw material space Sm is formed below the bridge 5 by the repose angle surfaces 3b, 3b on both sides. Therefore, the raw material space S is formed by this space Sm and the space Sb inside the bridge 5.
【0017】また、図2に示すように、ブリッジ5の下
方の原料通路2の内筒1(外筒2)の直径方向(原料通
路2の幅方向)には熱ガス流出口7の作用で傾斜した原
料上面3cが形成され、原料空間Sはこの上面3cの上
で原料通路2の幅方向にも延びて形成される。そして、
この原料空間Sに原料通路2の幅方向に連通して熱ガス
流出口7が位置されている。即ち、図3にも示すよう
に、熱ガス流出口7はその幅はブリッジ5の両側の袖5
cの間に位置させた幅とされ、その高さも原料空間Sの
高さに相当した高さとされている。ブリッジ5はこのよ
うに熱ガス流出口7を覆うように形成されて取付けられ
る。Further, as shown in FIG. 2, the action of the lower raw material passage inner cylinder 1 of 2 (outer cylinder 2) in the radial direction (the raw material passage in the width direction 2) the hot gas stream exit 7 of the bridge 5 Is formed, and the raw material space S is formed on the upper surface 3c so as to extend also in the width direction of the raw material passage 2. And
A hot gas outlet 7 is located in communication with the raw material space S in the width direction of the raw material passage 2. That is, as shown in FIG. 3, the width of the hot gas outlet 7 is
c, and the height thereof also corresponds to the height of the raw material space S. The bridge 5 is formed and attached so as to cover the hot gas outlet 7 in this manner.
【0018】このような構成において、原料通路2の原
料充填層Aを通過して上昇してきた熱ガスは熱ガス流出
口7部分に至ると、ブリッジ5によって形成されたブリ
ッジ5下方の原料空間Sに流出し、ここを通って熱ガス
流出口7に流入して内筒1内に入り、原料充填層A外の
Bへと流れる。熱ガスに同伴されて浮遊するダストは原
料安息角面3b、3bや傾斜上面3cを通過した部分で
沈降し該原料安息角面3b、3bや傾斜上面3c上の原
料の上面に堆積して堆積ダストDとなり、原料の下降と
共に炉底に至り、製品取出口11から炉外へ排出され
る。In such a configuration, the hot gas which has risen through the raw material filling layer A of the raw material passage 2 reaches the hot gas outlet 7 and is formed by the raw material space S below the bridge 5 formed by the bridge 5. And flows into the hot gas outlet 7 to enter the inner cylinder 1 and flow to B outside the raw material packed bed A. Dust floating along with the hot gas settles at the portion passing through the raw material repose angle surfaces 3b, 3b and the inclined upper surface 3c and deposits on the upper surface of the raw material on the raw material repose angle surfaces 3b, 3b and the inclined upper surface 3c. It becomes dust D, reaches the furnace bottom with the descent of the raw material, and is discharged from the furnace through the product outlet 11.
【0019】なお、前記、熱ガスが原料空間Sから熱ガ
ス流出口7に流出するに際して、熱ガスはブリッジ5の
内部の空間Sbの天井面5dに衝突した後に熱ガス流出
口7の方向に向かうが、このとき熱ガスに同伴された一
部のダストは失速し、原料安息角面3b、3bや傾斜上
面3c上に沈降することにより、熱ガス流出口7側へ流
れるダスト量が減少される。なお、原料上面から熱ガス
流入口7の方向に延びてダストが溜まろうとしても原料
は耐えず下降しているため熱ガス流入口7が閉塞するこ
とが防がれる。このように、焼成炉の操業を中断して堆
積ダストの除去作業を行う必要がなくなり、効率の良い
操業を可能とすることができる。When the hot gas flows out of the raw material space S to the hot gas outlet 7, the hot gas collides with the ceiling surface 5d of the space Sb inside the bridge 5 and then flows in the direction of the hot gas outlet 7. At this time, some of the dust entrained by the hot gas stalls and settles on the material repose angle surfaces 3b, 3b and the inclined upper surface 3c, so that the amount of dust flowing to the hot gas outlet 7 side is reduced. You. In addition, even if the dust extends from the upper surface of the raw material toward the hot gas inlet 7 and the dust is likely to accumulate, the raw material does not endure and descends, so that the hot gas inlet 7 is prevented from being blocked. In this way, there is no need to interrupt the operation of the firing furnace to remove the accumulated dust, thereby enabling efficient operation.
【0020】[0020]
【0021】[0021]
【発明の効果】以上の説明から明らかなように、本発明
によれば、ブリッジの下部の原料空間において原料上面
に熱ガスに同伴されるダストを堆積させ、この堆積ダス
トを原料の流下を利用して熱ガス流出口位置から原料と
共に下降させて炉底から炉外へ排出することができるの
で、熱ガス流出口が堆積ダストによって閉塞されたりす
ることがなく、熱ガスを円滑に炉外へ流出させることが
できる。この場合において、本発明では、特に、熱ガス
に同伴されて熱ガス流出口へ向かおうとするダストの一
部を、ブリッジ内部空間の天井面に突き当たらせて失速
させ原料空間部の原料安息角面でなる原料上面に沈降さ
せ堆積させることができるので、該ブリッジ下部の原料
空間における原料上面へのダストの沈降、堆積をより有
効に行なわせることができ、熱ガス流出口へ流されるダ
スト量を有効に減少させることができる。また、ブリッ
ジ自体の下部分に熱ガス流出口に連通した内部空間を有
することにより、ブリッジによってブリッジの下方に形
成される原料安息角面でなる原料空間部とともに、熱ガ
ス流出口への熱ガスの排出通路を、確実に、かつ、広い
容積で確保することができ、熱ガスを確実に熱ガス流出
口へ排出させることができる。従って、従来のように炉
の操業を停止しなくてもよく、効率の良い操業を行うこ
とができるという優れた効果を奏することができる。As is apparent from the above description, according to the present invention, in the raw material space below the bridge, dust entrained by the hot gas is deposited on the upper surface of the raw material, and the deposited dust is used by utilizing the flow of the raw material. and so is lowered together with the raw material from the hot gas outlet positions can be discharged from the furnace bottom to the outside of the furnace, the hot gas outlet is no and child or closed by depositing dust, the hot gas smoothly outside the furnace Can be drained to In this case, in the present invention, in particular, the hot gas
Of dust that is accompanied by
Stalls against the ceiling of the bridge interior space
The material is settled on the upper surface of the raw material,
The material under the bridge can be deposited
More sedimentation and accumulation of dust on the upper surface of raw material in space
Can be effectively performed, and the
The amount of strike can be effectively reduced. Also,
There is an internal space in the lower part of the
By being shaped below the bridge by the bridge
Along with the raw material space formed by the material
Make sure that the hot gas discharge passage to the
The volume can be secured and the hot gas flows out reliably.
Can be discharged into the mouth. Therefore, it is not necessary to stop the operation of the furnace as in the related art, and an excellent effect that efficient operation can be performed can be obtained.
【図1】本発明の実施例の竪型焼成炉の全体構造を示す
縦断面図である。FIG. 1 is a longitudinal sectional view showing the entire structure of a vertical firing furnace according to an embodiment of the present invention.
【図2】図1の熱ガス流出口部の要部拡大縦断面図であ
り、図3のII〜II線矢視断面図である。FIG. 2 is an enlarged vertical sectional view of a main part of a hot gas outlet of FIG. 1, and is a sectional view taken along line II-II of FIG.
【図3】図2のIII〜III線矢視断面図である。FIG. 3 is a sectional view taken along line III-III in FIG. 2;
【図4】従来構造の竪型焼成炉の熱ガス流出口部の要部
を示す縦断面図である。FIG. 4 is a longitudinal sectional view showing a main part of a hot gas outlet part of a vertical firing furnace having a conventional structure.
1 内筒 2 原料通路 3、7 熱ガス流出口 3b 原料安息角面 4 原料 5 ブリッジ 6 外筒 A 原料充填層 B 原料充填層外 D 堆積ダスト S 原料空間部 Reference Signs List 1 inner cylinder 2 raw material passage 3, 7 hot gas outlet 3b raw material repose angle 4 raw material 5 bridge 6 outer cylinder A raw material packed layer B outside raw material packed layer D accumulated dust S raw material space
───────────────────────────────────────────────────── フロントページの続き (72)発明者 田本 幸義 千葉県市原市五井南海岸8番2号 株式 会社カルシード千葉工場内 (56)参考文献 特開 昭61−40851(JP,A) 特開 昭58−69389(JP,A) (58)調査した分野(Int.Cl.7,DB名) F27B 1/08 ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yukiyoshi Tamoto 8-2, Goi-minamikaigan, Ichihara-shi, Chiba In-house Calceed Chiba Plant (56) References JP-A-61-40851 (JP, A) 58-69389 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F27B 1/08
Claims (1)
筒の中央部に懸垂されて設けられた内筒とにより二重円
筒構造にされ、該外筒と内筒との間が焼成空間としての
円環状断面の原料通路とされてなり、該原料通路内で原
料充填層を下降させつつ下方からバーナで発生される熱
ガスを上昇させ向流接触させて原料の焼成を行うと共
に、熱ガスを該原料通路に面して該内筒の壁面に形成さ
れ該熱ガス発生用バーナよりも所定距離上方に位置した
熱ガス流出口を通して原料充填層から内筒の内部である
原料充填層外へ取り出すようにした竪型焼成炉におい
て、該熱ガス流出口の上部分の原料通路にブリッジを設
け、該ブリッジ自体にはその下部分にブリッジ内部空間
を形成し、該ブリッジによって該ブリッジの下方には該
ブリッジ内部空間の下方に引き続いて原料空間部を形成
させ、該ブリッジ内部空間と該原料空間部の両空間部が
該熱ガス流出口と連通される状態に構成し、該バーナで
発生された熱ガスは、原料通路の原料充填層を下方から
上方へ向けて流されて該ブリッジの下方の原料空間部に
ダストを伴って排出され、その後、該ブリッジ内部空間
の天井面に衝突して該熱ガス流出口へ流れうる構成にし
たことを特徴とする竪型焼成炉。1. An outer cylinder and an outer cylinder extending from an upper part to a lower part of the furnace.
A double circle with the inner cylinder suspended from the center of the cylinder
It has a cylindrical structure, and the space between the outer cylinder and the inner cylinder serves as a firing space.
It is the raw material passage annular cross-section, while lowering the material packed layer increases the hot gas generated by the burner from below by countercurrent contact with performing firing of the raw material in the raw material passage, the hot gas It is formed on the wall surface of the inner cylinder in surface to the material passage
Re vertical firing it was taken out into an interior of the inner cylinder <br/> material packed layer outside from the raw material packed layer through <br/> heat gas outlet located at a predetermined distance above the heat gas generation burner In the furnace, a bridge is provided in a raw material passage at an upper portion of the hot gas outlet, and a bridge internal space is provided at a lower portion of the bridge itself.
Is formed, and the bridge is provided under the bridge by the bridge.
Following below the bridge internal space to form a source space portion constitutes a state in which two spaces of the bridge interior space and raw material space portion communicates with the <br/> heat gas outlet, in the burner
The generated hot gas passes through the raw material packed bed in the raw material passage from below.
Flowed upward and into the raw material space below the bridge
Discharged with dust, then the bridge interior space
A vertical firing furnace characterized in that the vertical firing furnace has a structure capable of colliding with a ceiling surface of the furnace and flowing to the hot gas outlet .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4313900A JP3038338B2 (en) | 1992-10-13 | 1992-10-13 | Vertical firing furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4313900A JP3038338B2 (en) | 1992-10-13 | 1992-10-13 | Vertical firing furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06129769A JPH06129769A (en) | 1994-05-13 |
| JP3038338B2 true JP3038338B2 (en) | 2000-05-08 |
Family
ID=18046872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4313900A Expired - Lifetime JP3038338B2 (en) | 1992-10-13 | 1992-10-13 | Vertical firing furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3038338B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100878625B1 (en) * | 2002-08-06 | 2009-01-15 | 주식회사 포스코 | Automatic removal device of sediment dust inside the dust collecting pipe |
-
1992
- 1992-10-13 JP JP4313900A patent/JP3038338B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06129769A (en) | 1994-05-13 |
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